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JPH0510970B2 - - Google Patents
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JPH0510970B2 - - Google Patents

Info

Publication number
JPH0510970B2
JPH0510970B2 JP61094172A JP9417286A JPH0510970B2 JP H0510970 B2 JPH0510970 B2 JP H0510970B2 JP 61094172 A JP61094172 A JP 61094172A JP 9417286 A JP9417286 A JP 9417286A JP H0510970 B2 JPH0510970 B2 JP H0510970B2
Authority
JP
Japan
Prior art keywords
metal
impact
particles
powder
spreading
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP61094172A
Other languages
Japanese (ja)
Other versions
JPS62250942A (en
Inventor
Yorioki Nara
Masumi Koishi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nara Machinery Co Ltd
Original Assignee
Nara Machinery Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nara Machinery Co Ltd filed Critical Nara Machinery Co Ltd
Priority to JP61094172A priority Critical patent/JPS62250942A/en
Priority to DE8686112228T priority patent/DE3687219T2/en
Priority to EP86112228A priority patent/EP0224659B1/en
Priority to SU864028279A priority patent/RU2047362C1/en
Priority to CN 86106765 priority patent/CN1007127B/en
Priority to KR1019860010468A priority patent/KR900001366B1/en
Publication of JPS62250942A publication Critical patent/JPS62250942A/en
Priority to US07/183,297 priority patent/US4915987A/en
Publication of JPH0510970B2 publication Critical patent/JPH0510970B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/75Discharge mechanisms
    • B01F35/754Discharge mechanisms characterised by the means for discharging the components from the mixer
    • B01F35/7547Discharge mechanisms characterised by the means for discharging the components from the mixer using valves, gates, orifices or openings
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/16Auxiliary treatment of granules
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50Mixing liquids with solids
    • B01F23/565Mixing liquids with solids by introducing liquids in solid material, e.g. to obtain slurries
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/70Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80Mixing plants; Combinations of mixers
    • B01F33/836Mixing plants; Combinations of mixers combining mixing with other treatments
    • B01F33/8363Mixing plants; Combinations of mixers combining mixing with other treatments with coating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7173Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper
    • B01F35/71731Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper using a hopper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/006Coating of the granules without description of the process or the device by which the granules are obtained
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/60Mixing solids with solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/16Auxiliary treatment of granules
    • B29B2009/163Coating, i.e. applying a layer of liquid or solid material on the granule

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Glanulating (AREA)
  • Manufacturing Of Micro-Capsules (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Pigments, Carbon Blacks, Or Wood Stains (AREA)
  • Powder Metallurgy (AREA)
  • Conductive Materials (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、核となる粒子(以下母粒子という)
の表面にあらかじめ金属微粒子(以下子粒子とい
う)を付着させておくか、又は付着させずにお
き、該金属子粒子を母粒子の表面に固着し、さら
に該金属子粒子全部あるいは一部を衝撃式打撃手
段で延展させて、母粒子の表面へ金属を延展固定
する方法に関する。 従来、一般に固体粒子の固結防止、変色変質防
止、分散性の向上、流動性の改善、触媒効果の向
上、消化・吸収の制御、磁気特性の向上、色調の
改善、耐光性の向上、有用(高価)物質の省量化
などを目的として各種の表面改質が、電気化学的
方法、物理吸着法、化学吸着法、真空蒸着法、静
電付着法、溶解物質の被覆法、特殊スプレードラ
イング法などの方法で行なわれて来た。これらの
うち、特に固体粒子の表面を金属固体粒子で、即
ち、粉体の表面を金属粉体で表面改質する場合
は、公知の各種ミキサー型やボールミル型の撹拌
機を使つて長時間(数時間〜数十時間)撹拌し、
撹拌に伴なつて生ずる静電現象やメカノケミカル
現象を応用して改質を行なつて来たが、母粒子の
囲りに金属子粒子が付着するだけで母粒子に対す
る子粒子の密着性が十分でなく、そのため改質後
の粉体を次工程で混合、混練、分散、ペースト化
等の加工をする場合、子粒子が簡単に脱落した
り、成分偏柝を生じたりしてその操作条件を著し
く制限するばかりでなく、加工後の生産品の品質
にバラツキが生じる最大の原因となつていた。 さらにまた、上記の各種ミキサー、ボールミル
等を使用した粉体−金属粉体系の表面改質にあつ
ては、一般に母粒子表面に対する子粒子の定着力
が弱いため、所望の表面改質を得るためには数時
間乃至数十時間を要し、そのため装置が大型とな
り、加工効率が決めて悪いなどの問題があつた。 本発明は前記事情に鑑みてなされたもので、従
来技術の問題点を解消し、第1図に示す如く、母
粒子の表面の一部または全域にわたつて金属子粒
子を機械的手段により、必要に応じて補助的手段
として熱的手段を用いて強制的に金属子粒子の全
部あるいは一部を延展させて固定化し、極めて短
時間(数秒〜数分間)のうちに均一な安定した粉
体粒子の表面改質を行ない、それによつて機能性
複合材料(ハイブリツドパウダー)を得ることが
できる方法を提供するもので、その要旨は、衝撃
室内に、衝撃ピンを周設した回転盤を配置すると
共に、該衝撃ピンの最外周軌道面に沿い、かつそ
れに対して一定の空間を置いて衝突リングを配置
し、前記衝撃ピンの回転によつて発生した気流
を、前記衝撃質と、前記衝突リングの一部から前
記回転盤の中心部付近の前カバーに開口する循環
回路とに誘導・循環させ、該気流と共に固体粒子
と、該固体粒子よりも小さな他の金属固体粒子と
から構成される粉対粒子群の全量を、前記循環回
路を介して繰り返し前記衝撃室に通過させ、前記
衝撃ピンと、前記衝突リングとの間で機械的打撃
により、前記固体粒子の表面に前記他の金属固体
粒子を固着させ、さらに継続した前記機械的打撃
により該金属固体粒子を延展させて固体化させる
ことを特徴とする固体粒子表面への金属の延展固
定方法にある。 本発明の方法で表面処理できる代表的母粒子粉
体としては、一般にその平均粒子径が0.1μm〜
100μm程度である炭酸カルシウム、カリオン、
アルミナ、けい砂、ガラスビーズ、二酸化チタン
等の無機物及び銅、鉛、亜鉛、スズ、鉄などの金
属並びに金属化合物及びエポキシパウダー、ナイ
ロンパウダー、ポリエチレンパウダー、ポリスチ
レンパウダーなどの有機物合成高分子材料、及び
デンプン、セルロース、シルクパウダーなどの有
機物天然材料であり、また、代表手金属子粒子粉
体(針状や糸状の場合もある)としては、一般に
粒径が0.01μm〜10μm程度であるところの金、
銀、銅、亜鉛、スズ、鉄、鉛、ステンレス、ニツ
ケル、アルミニウム、チタン、カドミウムなどの
微粉体及びこれらの酸化物粉体ならびに化合物粉
体などである。しかし、これらの粉体は、以上の
材料のみに限定されることなく、各種化学工業、
電気、磁気材料工業、化粧品、塗料、印刷イン
キ、及びトナー、色材、繊維、医薬、食品、ゴ
ム、プラスチツクス、窯業などの工業界で使用さ
れている各種材料の各組合わせ成分に適用するこ
とができる。 なお、一般に母粒子として大粒径のもの、子粒
子として小粒径のものを用いるが、材料粒子の大
きさの組合わせによつては、母粒子の子粒子が逆
になることもある。 以下、本発明の実施例について図面を参照しな
がら詳細に説明する。 第2図及び第3図は衝撃式打撃手段として衝撃
式粉砕機を用いた例を示す。全図において、1は
本発明方法を実施するために使用する粉体衝撃装
置(代表的な衝撃式粉砕機)のケーシング、2は
その後カバー、3はその前カバー、4はケーシン
グ1内にあつて高速回転する回転盤、5は回転盤
4の外周に所定間隔を置いて放射状に周設された
複数の衝撃ピンであり、これは一般にハンマー型
またはプレート型のものである。6は回転盤4を
ケーシング1内に回転可能に軸支持する回転軸、
8は衝撃ピン5の最外周軌道面に沿い、かつそれ
に対して一定の空間を置いて周設された衝突リン
グであり、これは、各種形状の凹凸型または円周
平板型のものを用いる。9は衝突リングの一部を
切欠いて設けた改質粉体排出用の開閉弁で、これ
は場合によつては前カバーや後カバーの粉砕室に
面した一部を切欠いて設けてもよい。10は開閉
弁9の弁軸、11は弁軸10を介して開閉弁9を
操作するアクチユエーター、13は一端が衝突リ
ング8の内壁の一部に開口し、他端が回転盤4の
中心部付近の前カバーに開口して閉回路を形成す
る循環回路、14は原料ホツパー、15は原料ホ
ツパー14と循環回路13とを連結する原料供給
用のシユート、16は原料計量フイーダー、17
は原料貯槽である。18は回転盤4の外周と衝突
リング8との間に設けられた衝撃室、19は循環
回路13への循環口を夫々示す。20は改質粉体
排出シユート、21はサイクロン、22はロータ
リーバルブ、23はバツクフイルター、24はロ
ータリーバルブ、25は排風機、31はこの装置
の運転を制御する時限制御装置、32はあらかじ
め母粒子の表面に子粒子を付着させる必要のある
場合に使用する各種ミキサー、電動乳鉢等公知の
プレプロセツサーを夫々示す。 上記装置を用いて、本発明の方法を実施する場
合、次の要領で操作する。 まず、改質粉体排出用の開閉弁9を閉鎖した状
態としておき、空気または必要に応じて不活性ガ
スを装置内に導入しながら、駆動手段(図示せ
ず)によつて回転軸6を駆動し、改質処理すべき
物質の性質により5m/sec〜160m/secの周速
度で回転盤4を回転させる。この際、回転盤4外
周の衝撃ピン5の回転に伴つて急激な空気・不活
性ガスの気流が生じ、この気流の遠心力に基づく
フアン効果によつて衝撃室18に開口する循環回
路13の循環口19から循環回路13を巡つて回
転盤4の中心部に戻る気流の循環流れ、即ち完全
な自己循環の流れが形成される。しかもこの際発
生する単位時間当りの循環風量は、衝撃室と循環
系の全容積に較べて著しく多量であるため、短時
間のうちに莫大な回数の気流循環サイクルが形成
されることになる。 次に、一定量の母粒子の表面に例えば静電現象
を利用して子粒子を付着させた被処理粉体また
は、若干の水または各種の有機溶剤などのバイン
ダーとなる物性を介在させて母粒子の表面に子粒
子を付着させた被処理粉体を、計量フイーダー1
6より原料ホツパー14に短時間で投入する。プ
レプロセツサー32を使用する必要のない場合
は、母粒子、子粒子並びに若干のバインダーを
夫々別々に計量して原料ホツパー14に投入す
る。被処理粉体は原料ホツパー14からシユート
15を通り衝撃室18に入る。衝撃室18へ送入
された粉体粒子群は、ここで高速回転する回転盤
4の多数の衝撃ピン5によつて瞬間的な打撃作用
を受け、さらに周辺の衝突リング8に衝突して母
粒子表面の全属子粒子が選択的に強度の圧縮作用
を受ける。そして同時に前記循環ガスの流れに同
伴して被処理粉体は循環回路13を循環して再び
衝撃室18へ戻り、再度打撃作用を受ける。 この様な衝撃作業が短時間のうちに連続して何
回も繰り返され、金属子粒子は母粒子の表面に強
力に延展され、さらに、衝撃、打撃作用による
(熱)エネルギーを受けることにより、該金属子
粒子は短時間のうちに母粒子表面へ強固に固着さ
れる。そしてこの一連の衝撃作業、即ち母粒子表
面に対する金属子粒子の延展固定化作業は、母粒
子の全表面が局所的あるいは全面的に所望の延展
固定化状態になるまで継続させるが、衝撃室と循
環系の全容積に較べて多量のガス(空気及び不活
性ガス)が系内を循環するため、ガスと同伴して
循環する被処理粉体(母粒子と金属子粒子)は極
めて短時間のうちに莫大な衝撃回数を受けること
になる。一回分の処理量にもよるが、この延展固
定化に要する時間は被処理粉体の供給時間を含め
ても一般に数秒乃至数分の極めて短時間内で終了
する。 第1図にモデル図を示す。図において母粒子、
金属子粒子は球状に限定されない。全図1,2は
母粒子a,a′に金属子粒子b,b′を予め静電気ま
たは極微量のバインダーにより付着させた状態を
示すが、これらの母粒子、金属子粒子は上記衝
撃、打撃作用により同図3〜5に示すように金属
子粒子の表面が延展され、金属子粒子同志の接着
あるいは重なり合いが一部あるいは全面に生じ、
固定化される。また金属子粒子の多種組合せや、
供給順序によつては同図6〜8に示す様に、母粒
子aに互いに異なる金属子粒子b,cを単層や多
層に延展固定化することができる。 以上の延展固定化作業が終了した後は、処理粉
体排出用の開閉弁9を鎖線で示す位置に移動させ
て開き、処理された粉体を排出する。この延展固
定化処理された粉体は、それ自身に作用している
遠心力(処理粉体に遠心力が作用しているところ
であれば排出弁9の位置は別のところでも良い。)
と、排風機25の吸引力によつて短時間(数秒
間)で衝撃室18及び循環回路13から排出さ
れ、シユート20を通つてサイクロン21及び循
環回路13から排出され、シユート20を通つて
サイクロン21及びバツグフイルター23などの
粉末捕集装置に誘導された後捕集され、ロータリ
ーバルブ22,24を介して系外に排出される。 延展固定化処理された粉体を排出後、開閉弁9
は直ちに閉鎖され、再び計量フイダー16から、
次回以降の一定量の被処理粉体が衝撃室に供給さ
れて同様な工程を経て処理された粉体が次々と生
産される。なお、これら一連の回分固定化処理操
作は、関連機器の動作時間に関連して、予め時限
設定された時限制御装置31によつて制御され継
続される。 母粒子表面への金属子粒子の延展固定化が部分
的局部的固定化処理でよい場合は、第2図の粉体
衝撃装置をワンパス色の連続処理システムとして
使用することも出来る。その場合は第2図におけ
る循環口19を閉塞し、開閉弁9を開とした状態
で被処理粉体を原料ホツパー15から連続的に供
給すれば良い。 また、延展固定化処理操作中、熱的処理を補助
的に併用する必要のある場合(例えば母粒子と金
属子粒子の密着の度合いをより大きくする必要の
ある場合など)は、衝突リング8や循環回路13
をジヤケツト構造とし、各種の熱媒や熱媒を通し
て被処理粉体の延展固定化処理に都合のよい温度
条件を設定することができる。 また、本発明に用いる粉体衝撃装置において
は、前記回転盤4に補助羽根を装着し、あるいは
循環回路13の途中に、たとえば遠心力型プレー
トフアンなどを配置して循環流に更に強制力を与
えることもできる。すなわち、循環風量を増大さ
せれば単位時間内の循環回数が増加し、従つて粉
体粒子の衝突回数も増加するので、延展固定化処
理時間を短縮することができる。 さらにまた、本発明に用いる粉体衝撃装置は、
上述した循環回路を備えたもののみでなく、第2
図および第3図の装置において循環回路を取除い
た構造のものも、これを使用することができる。 次に本発明に用いる粉体衝撃装置において行な
う粉体作業においては、被処理粉体の延展固定化
中における酸化劣化を防止したり、発火や爆発を
防止する目的で窒素ガスなどの各種の不活性ガス
を使用する場合を説明する。 第4図は本発明に用いる粉体衝撃装置におい
て、この不活性ガスを使用する実施例を示す。な
おこの実施例の説明に際し、前記実施例と同一部
材については同一符号を付し、説明を省略する。
第4図において、26は原料ホツパー14の下部
に設けた原料供給弁、27は原料供給用のシユー
ト15に開口する不活性ガスの供給弁、28は不
活性ガス供給源、29は不活性ガスの供給路を示
す。尚、この実施例では循環回路13をケーシン
グ1内に収納した態様を示す。 運転開始に際して、まず、原料供給弁26を閉
じ、開閉弁9を開いたあと、不活性ガスの供給弁
27を開き衝撃室18及び循環回路13内に不活
性ガスを充満させておく。この固定化作業開始に
先立つて行なう衝撃室及び循環回路内への不活性
ガスの置換は、通常数分以内で終了する。 次に開閉弁9と供給弁27とを同時に閉じたあ
と、直ちに原料供給弁26を開いて、予め計量さ
れた被処理粉体をシユート15を通じて衝撃室1
8に供給する。なお供給後、供給弁26は直ちに
閉の状態に戻し、その信号を受けて計量フイーダ
ー16は原料ホツパー14に次回の被処理粉体を
計量し供給しておく。 以後は、不活性ガスと共に前記実施例の場合と
同様に被処理粉体の衝撃を行ない、被処理粉体は
循環回路13内を循環しながら不活性ガスとの十
分な接触を保ちつつ延展固定化処理される。次に
開閉弁9と供給弁27とを開くと延展固定化処理
された粉体は、衝撃室18及び循環回路13から
シユート20へ排出され、同時に衝撃室18及び
循環回路13は新らしい不活性ガスで置換され
る。排出された延展固定化粉体は前記実施例と同
様に処理される。 以後は開閉弁9及び供給弁27を閉じて原料供
給弁26を開とすれば、次回分の延展固定化処理
操作が進行する。なお、不活性ガスの供給、停止
を含むこれら一連の回分固定化操作は、前記実施
例と同様に時限制御装置31によつて制御され継
続される。 なお母粒子表面への金属子粒子固定化が局所的
部分の延展固定化処理でよい場合は、第4図の粉
体衝撃装置をワンパス色の連続処理システムとし
て使用することができる。その場合は第4図にお
ける循環回路13を閉塞し、原料供給弁26及び
不活性ガスの供給弁27並びに開閉弁9を開とし
た状態で被処理粉体を原料ホツパー14から連続
的に一定量の割合で供給すればよい。この際、排
風機(第2図の25)出口の不活性ガスを原料供
給シユート15へ戻す方式を採れば不活性ガスの
使用量を節減することになり経済的である。 上述の如く、本願発明に係る固体(粉体)粒子
表面への金属の延展固定方法の特長は、衝撃式打
撃手段としての衝撃式粉砕機構の微小粉体粒子に
対する強力な衝撃力を利用することによつて、微
小粉体粒子を装置系内の気相中に完全に分散させ
た状態で、かつ一定の形状を有する母粒子の全表
面に付着させた金属子粒子に対する衝撃力付与の
ための衝撃力の大きさそれ自体及び衝撃回数を任
意に調節できることにある。従つて、凝集しやす
いミクロンオーダーの各種微小粉対相互の付着を
完全に防止しつつ、同時に微小粉体の1個、1個
に対して過不足のない打撃力を付与することがで
きるため一様な品質の、しかも金属特有の色、輝
きなど発色性のよい改質粉体を短時間のうちに生
産することができる。 また、第1図に示す如く本発明の方法によれ
ば、各種材料の母粒子に対する金属子粒子の延展
固定化は単なる一成分金属子粒子による単粒子層
の延展固定化処理にとどまらず、母粒子を膜状に
被服するマイクロカプセル化、二成分以上の金属
子粒子の延展固定化、さらには一成分以上の金属
子粒子による複数層に延展固定化処理することが
できる。また金属子粒子の形状も球状、不定形、
繊維状などのその形状はとわない。 また、本発明の方法によれば、各母粒子に対す
る延展固定化金属子粒子の割合(比率)がそれ程
厳密でなくともよい場合(即ち、全体としての成
分比率が一定であればよい場合)は、各種ミキサ
ー、電動乳鉢などのプレプロセツサーを使用せ
ず、別々に計量された母粒子粉体と金属子粒子粉
体を直接衝撃室に供給して母粒子表面に対する金
属子粒子の延展固定化処理を行なうことができ
る。 以上のように、本願発明に係る方法によれば、
各種粉体材料の組合わせから成る母粒子に対して
金属子粒子を延展固定化させる表面の改質処理を
行ない、均一で安定した特性を有する機能性複合
混成粉体材料(コンポジツトまたはハイブリツド
パウダー)を極めて短時間で効率よく生産するこ
とができる。 実施例 1 回転盤に周設された8枚のプレート型衝撃ピン
の外径が235mm、循環回路の直径が54.9mmである
第2図の粉体衝撃装置を使用した。母粒子として
平均粒径dp50=15μmの球状ナイロン12の表面に
平均粒径dp50=0.5〜3μmの導電塗料用銀粉子粒
子をあらかじめミキサーで付着させたオーダード
ミクスチヤーを夫々下表に示す処理条件で延展固
定化処理した結果、何れも導電塗料用銀粉(金属
子粒子)がナイロン12(母粒子、核粒子)の表面
に延展固着し、均一安定したナイロン12の導電塗
料用銀粉による表面改質粉体を得た。
The present invention focuses on core particles (hereinafter referred to as base particles).
Either fine metal particles (hereinafter referred to as child particles) are attached to the surface of the mother particle in advance or they are not attached to the surface of the mother particle, and the metal child particles are fixed to the surface of the mother particle, and then all or part of the metal child particles are subjected to impact. This invention relates to a method of spreading and fixing metal onto the surface of base particles by spreading with a type impact means. Conventionally, it has generally been used to prevent caking of solid particles, prevent discoloration and deterioration, improve dispersibility, improve flowability, improve catalytic effect, control digestion and absorption, improve magnetic properties, improve color tone, improve light resistance, and be useful. Various surface modifications are used to reduce the amount of (expensive) substances used, including electrochemical methods, physical adsorption methods, chemical adsorption methods, vacuum evaporation methods, electrostatic deposition methods, coating methods for dissolved substances, and special spray drying methods. It has been done in such a way. Among these, in particular, when the surface of solid particles is modified with metal solid particles, that is, the surface of powder is modified with metal powder, it is necessary to modify the surface of solid particles with metal powder for a long time ( Stir for several hours to several tens of hours,
Modification has been carried out by applying the electrostatic and mechanochemical phenomena that occur with stirring, but the adhesion of the child particles to the mother particle is reduced by simply adhering the metal child particles around the mother particle. Therefore, when the modified powder is mixed, kneaded, dispersed, made into a paste, etc. in the next process, the child particles may easily fall off or the ingredients may be unbalanced, resulting in poor operating conditions. Not only did this significantly limit the quality of the product, but it was also the biggest cause of variations in the quality of processed products. Furthermore, in surface modification of powder-metal powder systems using the above-mentioned various mixers, ball mills, etc., since the fixing force of child particles to the mother particle surface is generally weak, it is difficult to obtain the desired surface modification. This process requires several hours to several tens of hours, resulting in large equipment and problems such as poor processing efficiency. The present invention has been made in view of the above-mentioned circumstances, and solves the problems of the prior art.As shown in FIG. If necessary, thermal means can be used as an auxiliary means to forcibly spread and fix all or part of the metal particles, creating a uniform and stable powder in an extremely short period of time (several seconds to several minutes). This provides a method for surface-modifying particles and thereby obtaining a functional composite material (hybrid powder).The gist of the method is to place a rotating disk surrounded by impact pins in an impact chamber. At the same time, a collision ring is arranged along the outermost orbital surface of the impact pin and with a certain space therebetween, and the airflow generated by the rotation of the impact pin is directed between the impact material and the impact ring. A powder composed of solid particles and other metal solid particles smaller than the solid particles is guided and circulated from a part of the rotary disk to a circulation circuit that opens in the front cover near the center of the rotary disk, and together with the air flow, a powder consisting of solid particles and other metal solid particles smaller than the solid particles is The entire amount of the anti-particle group is repeatedly passed through the impact chamber via the circulation circuit, and the other metal solid particles are applied to the surface of the solid particles by mechanical impact between the impact pin and the collision ring. The present invention provides a method for spreading and fixing metal onto the surface of solid particles, which comprises fixing the solid particles, and then spreading and solidifying the solid metal particles by the continuous mechanical impact. Typical base particle powders that can be surface-treated by the method of the present invention generally have an average particle diameter of 0.1 μm to
Calcium carbonate, carrion, which is about 100μm
Inorganic materials such as alumina, silica sand, glass beads, and titanium dioxide; metals such as copper, lead, zinc, tin, and iron; and metal compounds; and organic synthetic polymer materials such as epoxy powder, nylon powder, polyethylene powder, and polystyrene powder; They are organic natural materials such as starch, cellulose, and silk powder, and representative metal particle powders (sometimes acicular or thread-like) include gold, which generally has a particle size of about 0.01 μm to 10 μm. ,
These include fine powders of silver, copper, zinc, tin, iron, lead, stainless steel, nickel, aluminum, titanium, cadmium, and their oxide powders and compound powders. However, these powders are not limited to the above materials, but are also used in various chemical industries,
Applicable to various combinations of materials used in industries such as electricity, magnetic materials, cosmetics, paints, printing inks, toners, colorants, textiles, pharmaceuticals, foods, rubber, plastics, and ceramics. be able to. Generally, large-sized parent particles and small-sized child particles are used as the parent particles, but depending on the combination of material particle sizes, the child particles of the parent particles may be reversed. Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. FIGS. 2 and 3 show an example in which an impact type crusher is used as the impact type striking means. In all the figures, 1 is the casing of the powder impact device (typical impact crusher) used to carry out the method of the present invention, 2 is the rear cover, 3 is the front cover, and 4 is the inside of the casing 1. A rotary disk 4 rotates at high speed, and reference numeral 5 denotes a plurality of impact pins radially arranged around the outer periphery of the rotary disk 4 at predetermined intervals, and these are generally hammer-shaped or plate-shaped. 6 is a rotary shaft that rotatably supports the rotary disk 4 within the casing 1;
Reference numeral 8 denotes a collision ring which is disposed around the outermost orbital surface of the impact pin 5 and with a certain space therebetween, and this can be of various concave and convex shapes or of a circumferential flat plate type. Reference numeral 9 denotes an on-off valve for discharging modified powder, which is provided by cutting out a part of the collision ring, and in some cases, this may be provided by cutting out a part of the front cover or rear cover facing the grinding chamber. . 10 is a valve shaft of the on-off valve 9; 11 is an actuator that operates the on-off valve 9 via the valve shaft 10; 13 has one end opening into a part of the inner wall of the collision ring 8; and the other end opening into the rotary disk 4. A circulation circuit that opens in the front cover near the center to form a closed circuit, 14 a raw material hopper, 15 a raw material supply chute connecting the raw material hopper 14 and the circulation circuit 13, 16 a raw material measuring feeder, 17
is the raw material storage tank. Reference numeral 18 indicates a shock chamber provided between the outer periphery of the rotary disk 4 and the collision ring 8, and reference numeral 19 indicates a circulation port to the circulation circuit 13. 20 is a modified powder discharge chute, 21 is a cyclone, 22 is a rotary valve, 23 is a back filter, 24 is a rotary valve, 25 is an exhaust fan, 31 is a time control device for controlling the operation of this device, and 32 is a preset Various types of mixers, electric mortars, and other known preprocessors used when it is necessary to attach child particles to the surface of particles are shown. When carrying out the method of the present invention using the above-mentioned apparatus, it is operated in the following manner. First, the on-off valve 9 for discharging the reformed powder is kept closed, and the rotating shaft 6 is moved by a driving means (not shown) while introducing air or an inert gas into the device as necessary. The rotary disk 4 is rotated at a circumferential speed of 5 m/sec to 160 m/sec depending on the nature of the substance to be modified. At this time, a rapid airflow of air/inert gas is generated as the impact pin 5 on the outer periphery of the rotary disk 4 rotates, and the circulation circuit 13 opens into the impact chamber 18 due to the fan effect based on the centrifugal force of this airflow. A circulating flow of air flows from the circulation port 19 through the circulation circuit 13 and back to the center of the rotary disk 4, that is, a completely self-circulating flow is formed. Furthermore, since the amount of circulating air generated per unit time is significantly larger than the total volume of the shock chamber and circulation system, an enormous number of air circulation cycles are formed in a short period of time. Next, a powder to be treated is prepared by attaching child particles to the surface of a certain amount of mother particles using electrostatic phenomenon, or a physical property that acts as a binder such as a small amount of water or various organic solvents is interposed to form a mother particle. The powder to be treated with child particles attached to the surface of the particles is transferred to the weighing feeder 1.
6, the raw material is fed into the hopper 14 in a short time. When it is not necessary to use the preprocessor 32, the mother particles, child particles, and some binder are weighed separately and charged into the raw material hopper 14. The powder to be processed passes from the raw material hopper 14 through the chute 15 and enters the shock chamber 18 . The powder particles sent into the impact chamber 18 are instantaneously impacted by a large number of impact pins 5 of the rotary disk 4 rotating at high speed, and further collide with the surrounding impact ring 8 to form a matrix. All metal particles on the particle surface are selectively subjected to strong compression. At the same time, the powder to be treated is circulated through the circulation circuit 13 along with the flow of the circulating gas, returns to the impact chamber 18, and is again subjected to the impact action. This type of impact operation is repeated many times in a row in a short period of time, and the metal particles are strongly spread on the surface of the base particle, and furthermore, by receiving (thermal) energy from the impact and impact action, The metal child particles are firmly fixed to the surface of the mother particle within a short time. This series of impact operations, that is, the work of spreading and fixing the metal particles on the surface of the base particle, is continued until the entire surface of the base particle is locally or completely brought into the desired spread and fixation state. Since a large amount of gas (air and inert gas) circulates in the system compared to the total volume of the circulation system, the powder to be processed (base particles and metal particles) that circulates with the gas is We will receive a huge number of shocks. Although it depends on the amount of treatment per batch, the time required for this spreading and fixing is generally completed within an extremely short time of several seconds to several minutes, even including the time for supplying the powder to be treated. Figure 1 shows a model diagram. In the figure, the mother particle,
The metal particle is not limited to a spherical shape. Figures 1 and 2 show a state in which metal particles b and b' are attached to base particles a and a' by static electricity or a very small amount of binder. As a result of the action, the surface of the metal particles is extended as shown in FIGS. 3 to 5, and adhesion or overlapping of the metal particles occurs partially or entirely.
Fixed. In addition, various combinations of metal particles,
Depending on the order of supply, as shown in FIGS. 6 to 8, different metal particles b and c can be spread and fixed in a single layer or in multiple layers on a base particle a. After the above spreading and fixing work is completed, the on-off valve 9 for discharging the treated powder is moved to the position shown by the chain line and opened, and the treated powder is discharged. This spread and immobilized powder is exposed to the centrifugal force acting on itself (as long as the centrifugal force is acting on the treated powder, the discharge valve 9 may be located at a different location).
Then, it is discharged from the shock chamber 18 and the circulation circuit 13 in a short period of time (several seconds) by the suction force of the exhaust fan 25, and is discharged from the cyclone 21 and circulation circuit 13 through the chute 20. 21 and a bag filter 23, the powder is collected and discharged to the outside of the system via rotary valves 22 and 24. After discharging the spread and immobilized powder, the on-off valve 9
was immediately closed, and from the weigh feeder 16 again,
A certain amount of powder to be treated from the next time onward is supplied to the impact chamber, and processed powder is produced one after another through the same process. Note that these series of batch fixing processing operations are controlled and continued by a time limit control device 31 whose time limit is set in advance in relation to the operating time of related equipment. If the spreading and immobilization of the metal particles onto the surface of the base particle requires partial local immobilization, the powder impacting device shown in FIG. 2 can also be used as a one-pass color continuous processing system. In that case, the powder to be treated may be continuously supplied from the raw material hopper 15 with the circulation port 19 in FIG. 2 closed and the on-off valve 9 open. In addition, when it is necessary to use supplementary thermal treatment during the spreading and fixing treatment operation (for example, when it is necessary to increase the degree of adhesion between the base particles and the metal particles), the collision ring 8 or Circulation circuit 13
By using a jacket structure, it is possible to set temperature conditions convenient for spreading and fixing the powder to be treated through various heating mediums and heating mediums. In addition, in the powder impacting device used in the present invention, auxiliary blades are attached to the rotary disk 4, or a centrifugal plate fan or the like is placed in the middle of the circulation circuit 13 to further apply force to the circulation flow. You can also give. That is, if the circulating air volume is increased, the number of times of circulation within a unit time increases, and therefore the number of collisions of powder particles also increases, so that the spreading and fixing processing time can be shortened. Furthermore, the powder impact device used in the present invention is
Not only the one equipped with the above-mentioned circulation circuit, but also the second
It is also possible to use the apparatuses shown in FIGS. 3 and 3 in which the circulation circuit is removed. Next, during the powder work performed in the powder impacting device used in the present invention, various impurities such as nitrogen gas are used to prevent oxidative deterioration during spreading and fixation of the powder to be processed, and to prevent ignition and explosion. The case of using active gas will be explained. FIG. 4 shows an example in which this inert gas is used in the powder impact device used in the present invention. In the description of this embodiment, the same members as in the previous embodiment are designated by the same reference numerals, and the explanation thereof will be omitted.
In FIG. 4, 26 is a raw material supply valve provided at the bottom of the raw material hopper 14, 27 is an inert gas supply valve that opens into the raw material supply chute 15, 28 is an inert gas supply source, and 29 is an inert gas supply valve. This shows the supply route. Note that this embodiment shows an embodiment in which the circulation circuit 13 is housed within the casing 1. When starting the operation, first, the raw material supply valve 26 is closed, the on-off valve 9 is opened, and then the inert gas supply valve 27 is opened to fill the shock chamber 18 and circulation circuit 13 with inert gas. The substitution of inert gas into the shock chamber and circulation circuit prior to the start of this immobilization work is usually completed within a few minutes. Next, after closing the on-off valve 9 and the supply valve 27 at the same time, the raw material supply valve 26 is immediately opened, and the pre-measured powder to be processed is passed through the chute 15 into the shock chamber 1.
Supply to 8. After supplying, the supply valve 26 is immediately returned to the closed state, and upon receiving this signal, the weighing feeder 16 measures and supplies the next powder to be processed to the raw material hopper 14. Thereafter, the powder to be treated is impacted with an inert gas in the same manner as in the above embodiment, and the powder to be treated is spread and fixed while circulating in the circulation circuit 13 while maintaining sufficient contact with the inert gas. processed. Next, when the on-off valve 9 and the supply valve 27 are opened, the powder that has been spread and fixed is discharged from the shock chamber 18 and circulation circuit 13 to the chute 20, and at the same time, the shock chamber 18 and circulation circuit 13 are replaced by gas. The discharged spread and fixed powder is treated in the same manner as in the previous example. Thereafter, by closing the on-off valve 9 and the supply valve 27 and opening the raw material supply valve 26, the next spreading and fixing treatment operation will proceed. Note that this series of batch fixing operations including supply and stop of the inert gas are controlled and continued by the time control device 31 as in the previous embodiment. If the fixation of the metal particles onto the surface of the base particle can be carried out by spreading and fixing the particles locally, the powder impacting device shown in FIG. 4 can be used as a one-pass color continuous processing system. In that case, the circulation circuit 13 shown in FIG. It is sufficient to supply it at a ratio of . At this time, if a method is adopted in which the inert gas at the outlet of the exhaust fan (25 in FIG. 2) is returned to the raw material supply chute 15, the amount of inert gas used can be reduced, which is economical. As mentioned above, the feature of the method for spreading and fixing metal on the surface of solid (powder) particles according to the present invention is that it utilizes the strong impact force on the fine powder particles of the impact type crushing mechanism as the impact type impact means. In order to apply an impact force to the metal particles attached to the entire surface of the base particle having a certain shape while the fine powder particles are completely dispersed in the gas phase in the device system, The reason is that the magnitude of the impact force itself and the number of impacts can be adjusted as desired. Therefore, it is possible to completely prevent various kinds of fine powders on the micron order, which tend to aggregate, from adhering to each other, and at the same time, it is possible to apply just the right amount of impact force to each of the fine powders. It is possible to produce modified powders of various quality in a short time, with good color development such as the color and shine unique to metals. Furthermore, as shown in FIG. 1, according to the method of the present invention, the spreading and fixing of metal particles to the mother particles of various materials is not limited to simply spreading and fixing a single particle layer using single-component metal particles; It is possible to perform microencapsulation in which the particles are coated in a film, spreading and fixing of metal particles of two or more components, and further spreading and fixing in multiple layers of metal particles of one or more components. In addition, the shape of the metal particle is spherical, irregular,
The shape, such as fibrous shape, is not limited. Furthermore, according to the method of the present invention, when the ratio (ratio) of the spread and immobilized metal child particles to each base particle does not need to be so strict (that is, when the overall component ratio only needs to be constant), , without using a preprocessor such as a mixer or an electric mortar, separately weighed base particle powder and metal particle powder are directly supplied to the impact chamber to spread and fix the metal particle onto the surface of the base particle. can be done. As described above, according to the method according to the present invention,
A functional composite powder material (composite or hybrid powder) that has uniform and stable properties by performing surface modification treatment to spread and fix metal particles on the base particles, which are made of a combination of various powder materials. can be produced efficiently in an extremely short time. Example 1 The powder impact device shown in FIG. 2 was used, in which the outer diameter of eight plate-type impact pins disposed around a rotary disk was 235 mm, and the diameter of the circulation circuit was 54.9 mm. Ordered mixers are prepared by adhering silver powder particles for conductive paints with an average particle size dp50 = 0.5 to 3 μm on the surface of spherical nylon 12 with an average particle size dp50 = 15 μm as base particles using a mixer, respectively, under the treatment conditions shown in the table below. As a result of the spreading and fixing treatment, the silver powder for conductive paints (metallic particles) was spread and fixed on the surface of Nylon 12 (base particles, core particles), resulting in uniform and stable surface modification of Nylon 12 with silver powder for conductive paints. A powder was obtained.

【表】 及び循環回路の内容積から算出した。
Calculated from [Table] and the internal volume of the circulation circuit.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図1〜8は本発明に係る方法による処理前
粉体と延展固定化後の粉体の各種態様を示す概念
的な説明図、第2図は、本発明に用いる粉体衝撃
装置の一例を、その前後装置とともに系統的に示
した概念的な説明図、第3図は第2図の側断面説
明図、第4図は同じく不活性ガスを用いる場合の
他の装置の説明図を示す。 a……母粒子、b,c……子粒子、1……衝撃
式粉砕機。
1 to 8 are conceptual explanatory diagrams showing various aspects of the powder before treatment and the powder after spreading and fixation according to the method according to the present invention, and FIG. 2 shows the powder impacting device used in the present invention. A conceptual explanatory diagram systematically showing one example along with its front and rear devices, Fig. 3 is a side cross-sectional explanatory diagram of Fig. 2, and Fig. 4 is an explanatory diagram of another device when using an inert gas. show. a... Mother particles, b, c... Child particles, 1... Impact type crusher.

Claims (1)

【特許請求の範囲】 1 衝撃室内に、衝撃ピンを周設した回転盤を配
置すると共に、該衝撃ピンの最外周軌道面に沿
い、かつそれに対して一定の空間を置いて衝突リ
ングを配置し、前記衝撃ピンの回転によつて発生
した気流を、前記衝撃室と、前記衝突リングの一
部から前記回転盤の中心部付近の前カバーに開口
する循環回路とに誘導・循環させ、該気流と共に
固体粒子と、該固体粒子よりも小さな他の金属固
体粒子とから構成される粉体粒子群の全量を、前
記循環回路を介して繰り返し前記衝撃室に通過さ
せ、前記衝撃ピンと、前記衝突リングとの間で機
械的打撃により、前記固体粒子の表面に前記他の
金属固体粒子を固着させ、さらに継続した前記機
械的打撃により該金属固体粒子を延展させて固定
化させることを特徴とする固体粒子表面への金属
の延展固定方法。 2 予め固体粒子と他の金属固体粒子とを混合
し、該固体粒子の表面に該他の金属固体粒子を付
着させておくことを特徴とする特許請求の範囲第
1項に記載の固体粒子表面への金属の延展固定方
法。 3 前記固体粒子の表面の隣合う前記金属固体粒
子の全部あるいは一部が、重なり合つて固定化さ
れることを特徴とする特許請求の範囲第1項に記
載の固体粒子表面への金属の延展固定方法。 4 補助手段として加熱して、前記固体粒子と前
記金属固体粒子相互を密着強化させることを特徴
とする特許請求の範囲第1項に記載の固体粒子表
面への金属の延展固定方法。 5 不活性ガス雰囲気下で上記延展固着工程を行
なうことを特徴とする特許請求の範囲第1項に記
載の固体粒子表面への金属の延展固定方法。
[Scope of Claims] 1. A rotary disk surrounding an impact pin is arranged in an impact chamber, and a collision ring is arranged along the outermost orbital surface of the impact pin and with a certain space therebetween. , the airflow generated by the rotation of the impact pin is guided and circulated through the impact chamber and a circulation circuit that opens from a part of the impact ring to the front cover near the center of the rotary disk; In addition, the entire amount of the powder particle group consisting of solid particles and other metal solid particles smaller than the solid particles is repeatedly passed through the impact chamber via the circulation circuit, and the impact pin and the collision ring are A solid characterized in that the other metal solid particles are fixed to the surface of the solid particles by mechanical impact between the solid particles, and the metal solid particles are further spread and immobilized by the continuous mechanical impact. A method for spreading and fixing metal onto particle surfaces. 2. The surface of the solid particle according to claim 1, characterized in that the solid particle and another metal solid particle are mixed in advance and the other metal solid particle is attached to the surface of the solid particle. Method of spreading and fixing metal to. 3. Spreading of metal on the surface of the solid particle according to claim 1, wherein all or part of the metal solid particles adjacent to each other on the surface of the solid particle overlap and are immobilized. Fixing method. 4. The method for spreading and fixing metal onto the surface of a solid particle according to claim 1, characterized in that heating is used as an auxiliary means to strengthen the adhesion between the solid particle and the metal solid particle. 5. The method for spreading and fixing metal onto the surface of solid particles according to claim 1, characterized in that the spreading and fixing step is carried out under an inert gas atmosphere.
JP61094172A 1985-05-07 1986-04-23 Method for spreading and fixing metal to surface of solid particle Granted JPS62250942A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP61094172A JPS62250942A (en) 1986-04-23 1986-04-23 Method for spreading and fixing metal to surface of solid particle
DE8686112228T DE3687219T2 (en) 1985-10-07 1986-09-04 METHOD FOR IMPROVING THE SURFACE QUALITY OF SOLID PARTICLES AND DEVICE THEREFOR.
EP86112228A EP0224659B1 (en) 1985-10-07 1986-09-04 Method of improving quality of surface of solid particles and apparatus thereof
SU864028279A RU2047362C1 (en) 1985-10-07 1986-10-03 Method and device for treating solid particle surface
CN 86106765 CN1007127B (en) 1985-05-07 1986-10-06 Method for improving quality of surface of solid particles and apparatus
KR1019860010468A KR900001366B1 (en) 1985-12-13 1986-12-08 Surface treating method of the solid particles and apparatus there for
US07/183,297 US4915987A (en) 1985-10-07 1988-04-11 Method of improving quality of surface of solid particles and apparatus thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61094172A JPS62250942A (en) 1986-04-23 1986-04-23 Method for spreading and fixing metal to surface of solid particle

Publications (2)

Publication Number Publication Date
JPS62250942A JPS62250942A (en) 1987-10-31
JPH0510970B2 true JPH0510970B2 (en) 1993-02-12

Family

ID=14102924

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61094172A Granted JPS62250942A (en) 1985-05-07 1986-04-23 Method for spreading and fixing metal to surface of solid particle

Country Status (1)

Country Link
JP (1) JPS62250942A (en)

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JPH0241210A (en) * 1988-08-01 1990-02-09 Calp Corp High function composite material and molded piece thereof
JP3386511B2 (en) * 1993-06-04 2003-03-17 浜口染工株式会社 Filler for colored resin molded product and method for producing the same
JP5011617B2 (en) * 2001-07-24 2012-08-29 住友ベークライト株式会社 Method for producing conductive resin particles
JP5011616B2 (en) * 2001-07-24 2012-08-29 住友ベークライト株式会社 Method for producing conductive resin particles
KR20070108798A (en) * 2006-05-08 2007-11-13 최길배 Polymer macroparticles surface-modified with nanoparticles and mesoparticles, nanoparticle-polymer composite materials using the same, and methods for their preparation
JP5072333B2 (en) * 2006-12-05 2012-11-14 株式会社トクヤマデンタル Processing method of organic-inorganic composite powder
JP4848540B2 (en) * 2007-02-16 2011-12-28 Dowaエコシステム株式会社 Metal powder for decomposing organohalogen compounds, method for producing the same, and method for purifying soil and the like using the same
JP5572913B2 (en) * 2008-01-17 2014-08-20 戸田工業株式会社 Conductive particle powder
JP5354569B2 (en) * 2008-09-05 2013-11-27 国立大学法人 千葉大学 Method for producing composite photocatalyst and composite photocatalyst produced thereby
JP5444699B2 (en) * 2008-11-28 2014-03-19 富士通株式会社 Conductive particles for anisotropic conductive adhesive, anisotropic conductive adhesive, method for producing conductive particles for anisotropic conductive adhesive, semiconductor device
JP2013026014A (en) * 2011-07-21 2013-02-04 Honda Motor Co Ltd Catalyst for fuel cell and manufacturing method of catalyst for fuel cell
CN104718579A (en) 2012-07-24 2015-06-17 株式会社大赛璐 Conductive fiber-coated particle, curable composition and cured article derived from curable composition
JP5573936B2 (en) * 2012-12-27 2014-08-20 戸田工業株式会社 Conductive particle powder
JP5585797B2 (en) * 2012-12-27 2014-09-10 戸田工業株式会社 Conductive particle powder

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5037631A (en) * 1973-08-06 1975-04-08

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